Hydrodynamic optimization of multi-environment reactors for biological nutrient removal: A methodology combining computational fluid dynamics and dimensionless indexes

被引:2
作者
Blanco-Aguilera R. [1 ]
Lara J.L. [2 ]
Barajas G. [2 ]
Tejero I. [1 ]
Díez-Montero R. [1 ,3 ]
机构
[1] Group of Environmental Engineering, Department of Water and Environmental Sciences and Technologies, University of Cantabria, Avenida los Castros s/n, Santander
[2] Environmental Hydraulics Institute (IHCantabria), University of Cantabria, Isabel Torres 15, Santander
[3] Group of Environmental Engineering and Microbiology, Department of Civil and Environmental Engineering, Universitat Politècnica de Catalunya, c/Jordi Girona 1-3, Building D1, Barcelona
关键词
Biological nutrient removal; Computational fluid dynamics; Dimensional analysis; Multi-environment; OpenFOAM®; Optimization;
D O I
10.1016/j.ces.2020.115766
中图分类号
学科分类号
摘要
Multi-environment reactors are an innovative alternative to simplify conventional Biological Nutrient Removal (BNR) treatment trains as they are more compact and can adapt to existing quality requirements. However, maintaining the desired environmental conditions in different zones of the reactor implies the need for deflectors or mixing devices that generate a complex hydrodynamic behaviour. Therefore, to ensure the desired biological efficiency, hydraulic optimization is essential. For that purpose, a hydrodynamic optimization methodology combining Computational Fluid Dynamics (CFD) and dimensional analysis is developed and presented in this work. The methodology is applied to AnoxAn, an anaerobic-anoxic reactor for BNR. The CFD model is constructed using the OpenFOAM® open source toolbox and has been already validated in a previous work by the authors. Different features as hydraulic separation, dead volumes, short-circuiting or mixing performance are evaluated and main results show that configurations of AnoxAn with high slenderness have the most efficient hydrodynamic behaviour. © 2020 Elsevier Ltd
引用
收藏
相关论文
共 55 条
[1]  
Angeloudis A., Stoesser T., Falconer R.A., Predicting the disinfection efficiency range in chlorine contact tanks through a CFD based approach, Water Res., 60, pp. 118-129, (2014)
[2]  
Arnaldos M., Rehman U., Naessens W., Amerlick Y., Nopens I., Understanding the effects of bulk mixing on the determination of the affinity index: Consequences for process operation and design, Water Sci. Technol., 77, 3, pp. 576-588, (2018)
[3]  
Blanco-Aguilera R., Lara J.L., Barajas G., Tejero I., Diez-Montero R., CFD simulation of a novel anaerobic-anoxic reactor for biological nutrient removal: Model construction, validation and hydrodynamic analysis based on OpenFOAM®, Eng. Sci. Chem., (2020)
[4]  
Buckingham E., On physically similar systems
[5]  
Illustrations of the use of dimensional equations, Physical Review, 4, pp. 345-376, (1914)
[6]  
Calder R.S.D., Yerushalmi L., Li S.S., Computational Fluid Dynamics model of BioCAST multienvironment air-lift bioreactor, J. Environ. Eng., 139, pp. 849-863, (2013)
[7]  
Castrillo M., Diez-Montero R., Esteban-Garcia A.L., Tejero I., Mass transfer enhancement and improved nitrification in MABR through specific membrane configuration, Water Res., 152, pp. 1-11, (2019)
[8]  
Celik I.B., Ghia U., Roache P.J., Freitas C.J., Coleman H., Raad P.E., Procedure for estimation and reporting of uncertainty due to discretization in CFD applications, J. Fluids Eng., 130, 7, (2008)
[9]  
Chang T.J., Chang Y.S., Lee W.T., Shih S.S., Flow uniformity and hydraulic efficiency improvement of deep-water constructed wetlands, Ecol. Eng., 92, pp. 28-36, (2016)
[10]  
Climent J., Basiero L., Martinez-Cuenca R., Berlanga J.G., Julian-Lopez B., Chiva S., Biological reactor retrofitting using CFD-ASM modelling, Chem. Eng. J., 348, pp. 1-14, (2018)